Continuous fermentative hydrogen production from coffee drink manufacturing wastewater by applying UASB reactor

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dc.contributor.authorJung, Kyung-Wonko
dc.contributor.authorKim, Dong-Hoonko
dc.contributor.authorShin, Hang-Sikko
dc.date.accessioned2013-03-11T00:52:51Z-
dc.date.available2013-03-11T00:52:51Z-
dc.date.created2012-02-06-
dc.date.created2012-02-06-
dc.date.issued2010-12-
dc.identifier.citationINTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.35, pp.13370 - 13378-
dc.identifier.issn0360-3199-
dc.identifier.urihttp://hdl.handle.net/10203/97848-
dc.description.abstractThe feasibility of continuous H(2) production from coffee drink manufacturing wastewater (CDMW) was tested in two different types of reactors: a completely-stirred tank reactor (CSTR) and an up-flow anaerobic sludge blanket reactor (UASBr). While the performance in CSTR was limited, it was significantly enhanced in UASBr. The maximum H(2) yield of 1.29 mol H(2)/mol hexose(added) was achieved at HRT of 6 h in UASBr operation. Non-hydrogenic, lactic acid was the dominant in CSTR, while butyric and caproic acids in UASBr. As caproic acid is generated by consuming acetic and butyric acids, all of which are related to H(2) production, the presence of caproic acid in the broth also indicates H(2) production, yielding 1.33 mo1 H(2)/glucose. It was speculated that the enhanced performance in UASBr was attributed to the high concentration of biomass over 60,000 mg VSS/L in the blanket zone, which provided insufficient substrate for indigenous lactic acid bacteria (LAB) to survive. The abundance of LAB in CDMW was confirmed by natural fermentation of CDMW. That is without the addition of external inoculum, CDMW was mainly fermented into lactic acid under mesophilic condition. For the first time ever, H(2) producing granules (HPG) with diameters of 2.1 mm were successfully formed by using actual waste as a substrate. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectSLUDGE BLANKET REACTOR-
dc.subjectBIOHYDROGEN PRODUCTION-
dc.subjectSTART-UP-
dc.subjectGRANULAR SLUDGE-
dc.subjectMIXED CULTURES-
dc.subjectPH-
dc.subjectOPERATION-
dc.subjectBACTERIA-
dc.subjectCALCIUM-
dc.subjectSYSTEMS-
dc.titleContinuous fermentative hydrogen production from coffee drink manufacturing wastewater by applying UASB reactor-
dc.typeArticle-
dc.identifier.wosid000284967100029-
dc.identifier.scopusid2-s2.0-78049475824-
dc.type.rimsART-
dc.citation.volume35-
dc.citation.beginningpage13370-
dc.citation.endingpage13378-
dc.citation.publicationnameINTERNATIONAL JOURNAL OF HYDROGEN ENERGY-
dc.identifier.doi10.1016/j.ijhydene.2009.11.120-
dc.embargo.liftdate9999-12-31-
dc.embargo.terms9999-12-31-
dc.contributor.localauthorShin, Hang-Sik-
dc.contributor.nonIdAuthorKim, Dong-Hoon-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorCSTR-
dc.subject.keywordAuthorUASBr-
dc.subject.keywordAuthorLAB-
dc.subject.keywordAuthorGranule-
dc.subject.keywordAuthorCaproic acid-
dc.subject.keywordAuthorLactic acid-
dc.subject.keywordPlusSLUDGE BLANKET REACTOR-
dc.subject.keywordPlusBIOHYDROGEN PRODUCTION-
dc.subject.keywordPlusSTART-UP-
dc.subject.keywordPlusGRANULAR SLUDGE-
dc.subject.keywordPlusMIXED CULTURES-
dc.subject.keywordPlusPH-
dc.subject.keywordPlusOPERATION-
dc.subject.keywordPlusBACTERIA-
dc.subject.keywordPlusCALCIUM-
dc.subject.keywordPlusSYSTEMS-
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